Preparation of (R)-3-hydroxybutyric acid or its salts by one-step fermentation

ABSTRACT

The subject invention relates to a process of preparing (R)-3-hydroxybutyric acid or a salt thereof by one-step fermentation with a nonpathogenic microorganism. The fermentation of (R)-3-hydroxybutyric acid was performed by supplying with certain carbon and nitrogen sources. These microorganisms include a Glutamic acid Bacterium HR057 strain or one type of genetically engineered  Corynebacterium Glutamicum.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional application of U.S. application Ser.No. 15/944,331, now U.S. Pat. No. 10,428,357, filed on Apr. 3, 2018,which claims priority to U.S. Application No. 62/481,476, filed on Apr.4, 2017, the contents of which are incorporated herein by reference intheir entirety.

TECHNICAL FIELD OF THE INVENTION

The subject invention pertains to the field of bioengineering, inparticular to a process for preparing (R)-3-hydroxybutyric acid and itssalts by microbial fermentation.

BACKGROUND OF THE INVENTION

(R)-3-hydroxybutyrate (3-HB) is an optically chiral compound with theCAS No. 625-72-9. (R)-3-hydroxybutyric acid is produced by themetabolism of long chain fatty acids in the liver of mammals. It existsas a major ketone in plasma and peripheral tissues and can be used as anenergy source in most tissues of the body.

(R)-3-hydroxybutyric acid has positive effect on treating many diseasesand nutritional functions as well. For example, it can be used to treatmany diseases that arise from elevated levels of ketone (such as nervedisorders including epilepsy and myoclonus, and neurodegenerativediseases including Alzheimer's disease and dementia); it can reduce freeradical damage by oxidizing the coenzyme Q (such as ischemia); it canenhance the efficiency of metabolism to achieve the treatment ofinadequate support, angina, myocardial infarction, etc. by improvingtraining efficiency and athletic performance; it can also be used totreat cancer related diseases such as brain cancer (astrocytoma, etc.).Further, it has good effects on the treatment of glucose metabolismdisorders (such as type-1 diabetes, type-2 diabetes, hypoglycemia ketonedisease, etc.). It can be used to control osteopenia (osteopenia),osteoporosis, severe osteoporosis and related fractures. Based on thesefunctions and therapeutic and nutritional effects, (R)-3-hydroxybutyricacid and its salts can be used as food additives and drugs with greathealth and medicinal values.

(R)-3-hydroxybutyric acid has been prepared primarily by chemicalmethods. It can be made from direct chemical synthesis or prepared byenzymatic degradation of poly-3-hydroxybutyrate withpoly-3-hydroxybutyric acid depolymerase. The chemical synthesis of(R)-3-hydroxybutyric acid requires a high temperature, a high pressureand expensive chiral metal catalysts. The process of enzymaticdegradation of poly-3-hydroxybutyric acid requires a large amount oforganic solvent, and very pure poly-3-hydroxybutyrate as startingmaterial. Besides the long reaction time, it is difficult to control theracemization of product after reaction. Moreover, this method needs moreoptimization in the laboratory to meet even higher requirements forindustrial scale commercialization because of high cost and lowefficiency.

At present, most of the commercially available 3-hydroxybutyric acid isa racemic mixture, with the ratio of (R)-3-hydroxybutyric acid to(S)-3-hydroxybutyric acid being about one to one. Although study showedthat (S)-3-hydroxybutyric acid is not physiologically active, racemic3-hydroxybutyric acid and its salts, especially sodium salts, are stillthe main commodity form and accepted by most consumers. It is expectedthat a single optical (R)-3-hydroxybutyric acid and its salts willbecome popular in future, replacing the racemic 3-hydroxybutyric acidand its salts.

Generally, it is believed that natural or biological compounds are safer(and non-toxic) than chemically produced compounds. People prefer the“natural” or “biological” feature of the source of pharmaceutical, foodand cosmetic ingredients. For marketing purpose, pharmaceuticals, food,and cosmetics manufacturers are more willing to replace chemical processwith biological process for making the same product. Therefore, therehas been a goal to produce (R)-3-hydroxybutyric acid in a biologicalmethod instead of a chemical method which is the main method.

BRIEF SUMMARY OF THE INVENTION

In order to produce “safe and nontoxic” (R)-3-hydroxybutyric acid in abiological method, inventors have studied various biological methods andunexpectedly found that fermentation procedures by nonpathogenicmicroorganism as the host were able to produce (R)-3-hydroxybutyric acidin an unusually efficient one-step process. Optimally engineeredorganisms have been screened and selected by genetic engineeringtechnology to enhance the expression of genes associated with(R)-3-hydroxybutyric acid main metabolic pathway and weaken the branchedmetabolic pathway. After that, (R)-3-hydroxybutyric acid can beeffectively accumulated in the fermentation process, which has broadapplication prospect in industrial scale.

Accordingly, in one aspect, this invention provides a biological processfor efficiently producing (R)-3-hydroxybutyric acid (e.g., in a one-stepmethod). In another aspect, this invention provides a food grade(R)-3-hydroxybutyric acid and salts thereof. In still another aspect,this invention also provides food grade racemic 3-hydroxybutyric acidand its salts to meet the needs of the market. In yet still anotheraspect, this invention further provides a bacterium which can ferment afermentation medium to produce (R)-3-hydroxybutyric acid.

Specifically, one aspect of the present invention provides a process forproducing (R)-3-hydroxybutyric acid comprising fermenting a fermentationbroth with a nonpathogenic microorganism. In this process, thefermentation broth comprises carbon and nitrogen sources and an enzymethat is overexpressed by the nonpathogenic microorganism, the carbon andnitrogen sources are directly converted into (R)-3-hydroxybutyric acidby one-step fermentation with the nonpathogenic microorganism, the(R)-3-hydroxybutyric acid was recovered from fermentation broth after itwas excreted during fermentation, the nonpathogenic microorganism isselected from a group consisting of Corynebacterium glutamicum, Bacillussubtilis, Brevibacterium lactofermentum, Brevibacterium difficile,Brevibacterium flavum and Brevibacterium breve; and the nonpathogenicmicroorganism has the following biotransformation capability: convertingpyruvic acid and coenzyme A to acetyl-CoA, converting acetyl-CoA intoacetoacetyl-CoA, converting acetoacetyl-CoA to acetoacetic acid, andconverting acetoacetic acid to (R)-3-hydroxybutyric acid.

In some embodiments, the enzyme overexpressed by the nonpathogenicmicroorganism comprises a member selected from the group consisting ofsuccinyl-CoA transferase, acetoacetyl-CoA synthase, and 3-HBdehydrogenase. In some prefer embodiments, the microorganismoverexpresses succinyl-CoA transferase and 3-HB dehydrogenase.

In some embodiments, the nonpathogenic microorganism comprisesCorynebacterium glutamicum, Glutamic acid Bacterium HR057, Bacillussubtilis, Brevibacterium lactofermentum, Brevibacterium difficile,Brevibacterium flavum, or Brevibacterium breve. In some preferredembodiments, the microorganism comprises Corynebacterium glutamicum orGlutamic acid Bacterium HR057. In some more preferred embodiments, themicroorganism is Corynebacterium glutamicum (such as that deposited atthe China General Microbiological Culture Collection Center under theaccession number CGMCC No. 13111).

In some embodiments, the carbon source comprises a member selected fromthe group consisting of glucose, sucrose, maltose, molasses, starch andglycerol. In some other embodiments, the nitrogen source comprises amember selected from the group consisting of an organic nitrogen sourceand an inorganic nitrogen source. Examples of suitable organic nitrogensource include, but are not limited to, corn steep liquor, branhydrolyzate, soybean cake hydrolyzate, yeast extract, yeast powder,peptone, and urea; wherein Examples of suitable inorganic nitrogensource include, but are not limited to, ammonium sulfate, ammoniumnitrate, and aqueous ammonia.

In some embodiments, the (R)-3-hydroxybutyric acid produced by theprocess of this invention is free of bacterial endotoxin and has apurity of 95% or more.

In some embodiments, the (R)-3-hydroxybutyric acid prepared by theprocess of this invention is in the form of (R)-3-hydroxybutyrate sodiumsalt, (R)-3-hydroxybutyrate potassium salt, (R)-3-hydroxybutyratemagnesium salt, or (R)-3-hydroxybutyrate calcium salt.

Another aspect of this invention provides a racemic 3-hydroxybutyricacid prepared by racemization treatment of the (R)-3-hydroxybutyric acidor a (R)-3-hydroxybutyrate salt produced in accordance of the process ofthis invention.

Another aspect of this invention provides a nonpathogenic microorganismwhich is selected from the group consisting of Corynebacteriumglutamicum, Glutamic acid Bacterium HR057, Bacillus subtilis,Brevibacterium lactofermentum, Brevibacterium difficile, Brevibacteriumflavum, and Brevibacterium breve.

In some embodiments, the nonpathogenic microorganism is aCorynebacterium glutamicum strain or a Glutamicacid Bacterium HR057strain. For instance, the Corynebacterium glutamicum strain is asdeposited at the China General Microbiological Culture Collection Centerunder the accession number CGMCC No. 13111.

In some preferred embodiments, the nonpathogenic microorganism iscapable of producing (R)-3-hydroxybutyric acid in a one-stepfermentation process of this invention.

The invention comprises the following technical scheme:

Fermentation of (R)-3-hydroxybutyric acid is carried out by using anon-pathogenic microorganism, which directly converts the carbon andnitrogen sources into (R)-3-hydroxybutyric acid which is excreted intothe fermentation broth and could be recovered directly. Themicroorganism can be one or more members selected from the groupconsisting of Corynebacterium glutamicum, Bacillus subtilis,Brevibacterium lactofermentum, Brevibacterium difficile, Brevibacteriumflavum and Brevibacterium breve. These microorganisms have the followingbiotransformation functions: converting pyruvic acid and coenzyme A toacetyl-CoA; converting acetyl-CoA into acetoacetyl-CoA; convertingacetoacetyl-CoA to acetoacetic acid; and then converting acetoaceticacid to (R)-3-hydroxybutyric acid.

Preferably, the microorganism over-expresses one or more enzymesselected from the group consisting of succinyl-CoA transferase,acetoacetyl-CoA synthase, and 3-HB dehydrogenase (3-HB Dehydrogenase,BDH).

More preferably, the microorganism overexpresses succinyl-CoAtransferase or 3-HB dehydrogenase.

Preferably, the microorganism inhibits or down regulates the expressionof β-ketothiolase.

In a preferred embodiment, the microorganism is Corynebacteriumglutamicum.

In another preferred embodiment, the Corynebacterium glutamicum is asdeposited at the China General Microbiological Culture Collection Centerunder the accession number CGMCC No. 13111.

Different media may be used for different microorganisms in thefermentation process. The carbon source may be selected from the groupconsisting of glucose, sucrose, maltose, molasses, starch and glycerol.One or more organic or inorganic nitrogen sources may be used in afermentation medium. The organic nitrogen source may come from the groupconsisting of corn steep liquor, bran hydrolyzate, soybean cakehydrolyzate, yeast extract, yeast meal, peptone and urea; and theinorganic nitrogen source may include one or more compounds selectedfrom the groups consisting of ammonium sulfate, ammonium nitrate, andaqueous ammonia.

In a preferred embodiment of the present invention, the fermentationmedium includes glucose 75 g/L, corn steep liquor 25-30 g/L, (NH₄)₂SO₄20 g/L, KH₂PO₄ 1.5 g/L, MgSO₄.7H₂O 0.5 g/L, urea 1.0 g/L, histidine 30mg/L, molasses 25 g/L, biotin 100 μg/L, and defoamer 0.2 g/L whenCorynebacterium glutamicum was applied.

Preferably, the feed medium includes ammonium sulfate 500 g/L andglucose 650 g/L when batch feed fermentation was performed.

The purity of the (R)-3-hydroxybutyric acid prepared by a fermentationmethod of the present invention could be greater than 95%, greater than96%, greater than 97%, greater than 98%, or even greater than 99%.

Pure (R)-3-hydroxybutyric acid thus prepared does not contain bacterialendotoxin and chemical odor such as bitterness.

(R)-3-hydroxybutyric acid is an acid which forms a salt with a base.Alternatively, the (R)-3-hydroxybutyric acid prepared by presentinvention may exist in the form of a salt, such as sodium salt,potassium salt, magnesium salt, or calcium salt, preferably in the formof a sodium salt. These salts may all be optically active compounds.

Since racemic 3-hydroxybutyric acid and its sodium salt havetraditionally been accepted by food and pharmaceutical manufacturers andconsumers, (R)-3-hydroxybutyric acid and its salts can be subjected toracemic treatment to prepare racemic 3-hydroxybutyric acid and itssalts. For example, racemization can be achieved by heating(R)-3-hydroxybutyric acid in an alkaline solution such as sodiumhydroxide solution for a certain time.

The racemic 3-hydroxybutyrate salt may be sodium 3-hydroxybutyrate,potassium 3-hydroxybutyrate, magnesium 3-hydroxybutyrate, or calcium3-hydroxybutyrate.

(R)-3-hydroxybutyric acid and its salts prepared by the presentinvention are free of bacterial endotoxin and toxic chemicals, thereforeensuring food safety. In addition, (R)-3-hydroxybutyric acid can be useddirectly to manufacture pharmaceuticals and health products as itcontains no chemical residues or chemical reaction impurities, and itdoes not have chemical odor such as bitterness as well.

The genetically engineered microorganisms constructed in the presentinvention can effectively produce and accumulate (R)-3-hydroxybutyricacid in the fermentation broth during the fermentation process, andcould give rise to food-grade (R) level by downstream process, which hasbroad industrial prospects.

Corynebacterium glutamicum has been engineered to produce(R)-3-hydroxybutyric acid at high yield. A strain of this microorganismhas been deposited under the accession number CGMCC No. 13111 on Oct.14, 2016, at China General Microbiological Culture Collection Center,located in Institution of Microbiology, Chinese Academy of Sciences,Building 3, No. 1 Beicheng West Road, Chaoyang District, Beijing, China100101.

As used herein, the term “one-step fermentation” refers to afermentation process that includes adding one or more fermenting agents(e.g., a microorganism) to a fermentation medium which is fermented togive the desired product, without having to add a second round offermenting agent and then going through a second round of fermentationprocess.

As used herein, the term “nonpathogenic microorganism” refers to amicroorganism that generally does not cause disease, harm or death toanother microorganism, an organism, or human being.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is further described in detail with specificembodiments. The following examples are intended to demonstrate theinvention and not to limit the scope of the invention.

Mass percentage is referred in the invention such as the added amount,content and concentration of multiple substances unless otherwiseprovided described or defined.

In the embodiments provided under the present invention, roomtemperature (15-30° C.) is referred to by default unless otherwiseprovided described or specified.

In the present invention, a microorganism strain capable of producing(R)-3-hydroxybutyric acid by fermentation is exemplified by but notlimited to “Corynebacterium glutamicum”, “Corynebacterium glutamicumstrain CGMCC No. 13111”, or “Glutamic acid Bacterium HR057”.

Fermentation of (R)-3-hydroxybutyric acid by microorganism wasinvestigated in the present invention in order to supply the consumerand pharmaceutical and food manufacturers with the “naturalized” or“biogenic” sources of (R)-3-hydroxybutyric acid and its salts,3-hydroxybutyric acid and its salts.

The inventors screened and selected species for the construction ofgenetic engineering strains. It is not considered that general strainwith potentially pathogenic feature such as Escherichia coli.Nonpathogenic microorganism was chosen and genetically engineered asfermentation strains such as Corynebacterium glutamicum, Bacillussubtilis, Brevibacterium lactofermentum, Brevibacterium difficile,Brevibacterium breve and Brevibacterium brevica. Several strains wereobtained through screening which are able to produce(R)-3-hydroxybutyric acid by fermentation. No endotoxin was produced atall during fermentation, which may cause harm to most people. So, it isconsidered as non-toxic and harmless” design.

It is necessary to adjust and control some parameters such as dissolvedoxygen, temperature, pH etc., to have a higher yield of(R)-3-hydroxybutyric acid during fermentation.

The constant dO2 is controlled at 15% to 25% during fermentation.Fermentation can be carried out under the following conditions: air flowis about 1 vvm, where vvm is the ratio of the amount of ventilation perminute to the actual volume of liquid in the tank (for example, 1 vvm isequal to 30 L/min for a fermenter containing 30 liters of fermentationbroth, and 1 vvm is equal to 5 L/min as for a fermentation tankcontaining 5 liters of fermentation broth,).

Preferably, the temperature is first controlled at 30˜32° C. during theinitial stage of fermentation and then increased to 34˜37° C. at thelater stage of the fermentation which facilitates the synthesis andexcretion of (R)-3-hydroxybutyric acid by the microorganism.

The pH is generally controlled at pH 6.0˜8.0, preferably at pH 6.5˜7.0,during the initial stage of fermentation. It can then be adjusted to6.8˜7.0 in the later stages of fermentation to facilitate the synthesisand drainage of (R)-3-hydroxybutyric acid from the fermentation broth.

The above term “later stage of fermentation” refers to from exponentialstage to stationary stage of microbial growth. For example, the OD600 nmvalue is no longer rising and tending to decrease when monitoring celldensity with OD600 nm values.

The residual sugar is controlled at 1.0%˜3.0% during fermentationprocess, more precisely at 1.5%˜2.5%.

After the fermentation is completed, the fermentation broth needs to berecovered and (R)-3-hydroxybutyric acid is extracted therefrom. Forexample, the supernatant of the fermentation broth is obtained bycentrifugation. The supernatant is concentrated if necessary;(R)-3-hydroxybutyric acid is separated by a post-treatment such aspurification and drying.

Cells and macromolecules in the fermentation medium can be removed byfiltration (including ultrafiltration, nanofiltration, etc.).Concentrated filtration, and other post-processing means such as drying,purification and other methods may be applied if necessary to isolate(R)-3-hydroxybutyric acid. Alternatively, (R)-3-hydroxybutyric acid canbe isolated by centrifugation which obtains supernatant of fermentationbroth, then go through ultrafiltration, nanofiltration and other methodsto remove macromolecules, or through concentrated filtration ifnecessary, then by drying, purification and other post-processing means.

To prepare (R)-3-hydroxybutyrate such as sodium salt, potassium salt,magnesium salt, calcium salt, an equivalent amount of(R)-3-hydroxybutyric acid is reacted with the corresponding base ormetal oxide such as sodium hydroxide. The reaction temperature iscontrolled to be 30° C. or lower, preferably at 25° C. or lower, andmore preferably at 20° C. or less, where the racemic reaction could beavoided as much as possible.

As the whole preparation process does not require or involve an organicsolvent, chemical odor like bitterness was not detected from the product(R)-3-hydroxybutyric acid which could be directly used to manufacturepharmaceuticals and health care products.

EXAMPLE 1 Pre-Culture and Fermentation

A glycerol stock CGMCC No. 13111 stored at −80° C. was thawed andinoculated to a 5000 mL flask containing 500 mL seed medium (75 g/L ofglucose, 25-30 g/L of corn steep liquor, 20 g/L of (NH₄)₂SO₄, 1.5 g/L ofKH₂PO₄, 0.5 g/L of MgSO₄.7H₂O, 1.0 g/L of urea, 30 mg/L of histidine, 25g/L of molasses, 100 μg/L of biotin, pH 7.0), and cultured at 30° C. for18 hours. The seed culture cultivation was completed when OD=0.4-0.5.

500 mL seed culture was inoculated into a 7-liter fermenter filled with5 liters medium. The composition of fermentation medium was the same asthe seed medium described above, and the pH was controlled at 6.4˜6.7after sterilization. Feed medium contains 500 g/L ammonium sulfate and650 g/L glucose. The fermentation temperature was set at 30° C., thetank pressure was kept at 0.05 Mpa, and the initial ventilation ratiowas 1 vvm. Stirring speed was 600 rpm. The pH of the fermentation wasabout pH 6.5.

The pH was controlled at 6.7 and the temperature was raised to 35° C. atthe later phase of fermentation. The dissolved oxygen constant (dO2) wascontrolled at 15˜25% by adjusting ventilation and stirring speed. Tocontrol residual sugar level, sugar was fed slowly while theconcentration of the original sugar dropped to about 3.0% and theresidual sugar was controlled at 1.5%˜2.0%. (R)-3-hydroxybutyric acidwas accumulated to 11.8 g/L after 72 hours.

EXAMPLE 2 Isolation of Fermentation Broth and Extraction of(R)-3-hydroxybutyric Acid

5.2 liters of the fermentation broth obtained in Example 1 wascentrifuged at 4500 rpm and the cells were discarded. The supernatantwas filtered with 1% diatomaceous earth. Clear filtrate was recoveredafter stirring for 30 minutes mixed with 1% activated carbon.

The filtrate was concentrated through nanofiltration membrane, and theresulting filtrate was passed through a 732 cation exchange resin to geta 1000 g/L concentrated filtrate. The concentrated collection was oilyand collected while hot to give 56.8 g of (R)-3-hydroxybutyric acid witha yield of 92.5%. The purity of (R)-3-hydroxybutyric acid was determinedby high performance liquid chromatography. The chromatographic columnwas Shim-pack Vp-ODSC18 column (150 L×4.6). The mobile phase consistedof acetonitrile: water (v/v)=15: 85, UV detection wavelength was 210 nm,injection volume was 20 μL, flow rate was 1 mL/min, column temperaturewas 10° C. The purity of (R)-3-hydroxybutyric acid was 98% and thespecific optical value was [α] D20=−25° (C=6%, H₂O).

EXAMPLE 3 Preparation of Sodium (R)-3-hydroxybutyrate

A neutralization reaction was performed by mixing 5 g of(R)-3-hydroxybutyric acid obtained in Example 2 with an equivalentamount of a 2.0 N sodium hydroxide solution at 25° C. or lower. 4.9 g ofsodium (R)-3-hydroxybutyrate powder was finally obtained with an 81%yield by rotating concentration, standing for 2 hours, and beingcollected by suction filtration and dried at 60° C. The salt has amelting point of 152° C. and a specific optical value [α] D20 of −14.1°(C=10%, H2O).

EXAMPLE 4 Racemization of (R)-3-hydroxybutyric Acid

10 g of (R)-3-hydroxybutyric acid was slowly added to 100 mL of a 2.0 Nsodium hydroxide solution, and the mixture was heated to 60° C. for 4hours. The optical value of product was 0° at room temperature. Aneutralization reaction was carried out by adding hydrochloric acid toadjust the pH of the mixture to 7.0. 10.3 g of sodium 3-hydroxybutyratepowder was obtained with a yield of 85% by rotary evaporation until asolid was observed, allowing to stand for 2 hours, and then filtration.The results showed that racemic 3-hydroxybutyrate was obtained.

In summary, the present invention disclosed that the engineeredCorynebacterium glutaricum by genetic modification could ferment(R)-3-hydroxybutyric acid in a one-step process at a high yield, whichwas proved to be safe and non-toxic food grade. The engineered strainand manufacturing process that were disclosed in this invention hasbroad industrial application prospects.

What is claimed is:
 1. A process for producing (R)-3-hydroxybutyricacid, wherein the process comprises culturing Corynebacterium glutamicumstrain deposited under the accession number CGMCC No. 13111 at the ChinaGeneral Microbiological Culture Collection Center in a fermentationbroth, wherein the fermentation broth comprises carbon and nitrogensources, and the carbon and nitrogen sources are directly converted into(R)-3-hydroxybutyric acid by a one-step fermentation, wherein the(R)-3-hydroxybutyric acid is recovered from the fermentation broth afterit is excreted during fermentation.
 2. The process of claim 1, whereinthe carbon source is selected from the group consisting of glucose,sucrose, maltose, molasses, starch and glycerol.
 3. The process of claim1, wherein the nitrogen source is selected from the group consisting ofan organic nitrogen source and an inorganic nitrogen source.
 4. Theprocess of claim 3, wherein the organic nitrogen source is selected fromthe group consisting of corn steep liquor, bran hydrolysate, soybeancake hydrolysate, yeast extract, yeast powder, peptone, and urea.
 5. Theprocess of claim 3, wherein the inorganic nitrogen source is selectedfrom the group consisting of ammonium sulfate, ammonium nitrate, andaqueous ammonia.
 6. The process of claim 1, wherein the(R)-3-hydroxybutyric acid is prepared in the form of(R)-3-hydroxybutyrate sodium salt, (R)-3-hydroxybutyrate potassium salt,(R)-3-hydroxybutyrate magnesium salt, or (R)-3-hydroxybutyrate calciumsalt.